US5827336A - Liquefaction and partial oxidation of plastic materials - Google Patents

Liquefaction and partial oxidation of plastic materials Download PDF

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Publication number
US5827336A
US5827336A US08/619,749 US61974996A US5827336A US 5827336 A US5827336 A US 5827336A US 61974996 A US61974996 A US 61974996A US 5827336 A US5827336 A US 5827336A
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United States
Prior art keywords
plastic
weight
gas
inorganic material
pumpable slurry
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Expired - Lifetime
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US08/619,749
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English (en)
Inventor
Motasimur Rashid Khan
Christine Cornelia Gorsuch
Stephen Jude DeCanio
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Texaco Inc
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Texaco Inc
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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46—Gasification of granular or pulverulent flues in suspension
    • C10J3/466—Entrained flow processes
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K1/00—Purifying combustible gases containing carbon monoxide
    • C10K1/08—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors
    • C10K1/10—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids
    • C10K1/101—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids with water only
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0903—Feed preparation
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0903—Feed preparation
    • C10J2300/0906—Physical processes, e.g. shredding, comminuting, chopping, sorting
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913—Carbonaceous raw material
    • C10J2300/0946—Waste, e.g. MSW, tires, glass, tar sand, peat, paper, lignite, oil shale
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/12—Heating the gasifier
    • C10J2300/1223—Heating the gasifier by burners
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/18—Details of the gasification process, e.g. loops, autothermal operation
    • C10J2300/1846—Partial oxidation, i.e. injection of air or oxygen only
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/18—Details of the gasification process, e.g. loops, autothermal operation
    • C10J2300/1861—Heat exchange between at least two process streams
    • C10J2300/1884—Heat exchange between at least two process streams with one stream being synthesis gas
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/18—Details of the gasification process, e.g. loops, autothermal operation
    • C10J2300/1861—Heat exchange between at least two process streams
    • C10J2300/1892—Heat exchange between at least two process streams with one stream being water/steam
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00—Technologies for wastewater treatment
    • Y02W10/40—Valorisation of by-products of wastewater, sewage or sludge processing
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S48/00—Gas: heating and illuminating
    • Y10S48/07—Slurry

Definitions

  • This invention relates to an environmentally safe method for disposing of scrap plastic materials. More particularly, it pertains to a process for upgrading scrap plastic materials to produce a pumpable slurry of hydrocarbonaceous liquid solvent and partially liquefied scrap solid carbonaceous plastic-containing material and introducing said slurry into a partial oxidation gasifier for the production of synthesis gas, reducing gas, or fuel gas.
  • Scrap plastics are solid organic polymers and are available in such forms as sheets, extruded shapes, moldings, reinforced plastics, laminates, and foamed plastics. About 60 billion pounds of plastics are sold in the United States each year. For example, automobiles are increasingly being manufactured containing more plastic parts. A large part of these plastic materials wind up as scrap plastics in landfills. Although plastics account for only a small portion of the waste dumped in landfills i.e. about 7 wt. % and about 20 percent by volume, burying them is getting increasingly difficult. The cost of landfilling this material in 1993 is between $12 to $100 per ton (excluding shipping costs); and this cost is rising. Landfills are not universally viewed as an acceptable, or even a tolerable option for the disposal of plastic materials.
  • plastic feedstocks are partially liquefied for volume reduction and comparatively low cost disposal by partial oxidation.
  • Useful synthesis gas, reducing gas or fuel gas is produced.
  • the relatively medium heating value of the plastic material e.g. greater than about 3,000 Btu/lb is made available for heating internal process streams or producing by-product hot water or steam.
  • This invention relates to an environmentally acceptable process for the partial oxidation of a pumpable slurry of hydrocarbonaceous liquid solvent and partially liquefied solid carbonaceous plastic material containing inorganic filler or reinforcement material; wherein synthesis gas, reducing gas, or fuel gas is produced by said process comprising the steps of:
  • Scrap plastics are disposed of by the process of the subject invention without polluting the nation's environment. Simultaneously, useful by-product nonpolluting synthesis gas, reducing gas, fuel gas and nonhazardous slag are produced.
  • the scrap plastic materials which are processed as described herein into a pumpable slurry fuel feed for a partial oxidation gas generator include at least one solid carbonaceous thermoplastic or thermosetting material that contains associated inorganic matter e.g. fillers and reinforcement material. Sulfur is also commonly found in scrap plastics. Scrap plastic materials may be derived from obsolete equipment, household containers, packaging, industrial sources and junked automobiles. The mixture of plastics is of varying age and composition. With the presence of varying amounts of incombustible inorganic matter compounded in the plastic as fillers, catalysts, pigments and reinforcing agents, recovery of the plastic material is generally impractical. Further, complete combustion can release toxic-noxious components including volatile metals and hydrogen halides.
  • Associated inorganic matter in the scrap solid carbonaceous plastic includes fillers such as titania, talc, clays, alumina, barium sulfate and carbonates.
  • Catalysts and accelerators for thermosetting plastics include tin compounds for polyurethanes, and cobalt and manganese compounds for polyesters.
  • Dyes and pigments such as compounds of cadmium, chromium, cobalt, and copper; non-ferrous metals such as aluminum and copper in plastic coated wire cuttings; metal films; woven and nonwoven fiber glass, graphite, and boron reinforcing agents; steel, brass, and nickel metal inserts; and lead compounds from plastic automotive batteries.
  • Other heavy metals e.g.
  • the inorganic constituents are present in the solid carbonaceous plastic-containing material in the amount of about a trace amount to about 60 wt. % of said solid carbonaceous plastic-containing material, such as about 1 to 20 wt. %.
  • the scrap plastic material may be in the form of sheets, extruded shapes, moldings, reinforced plastics, and foamed plastics.
  • the slurrying medium comprises a pumpable liquid hydrocarbonaceous solvent in the amount of about 30 to 90 wt. %.
  • liquid hydrocarbonaceous solvent as used herein to describe suitable liquid solvents is a liquid hydrocarbonaceous fuel selected from the group consisting of liquefied petroleum gas, petroleum distillates and residues, gasoline, naphtha, kerosine, crude petroleum, asphalt, gas oil, residual oil, tar sand oil and shale oil, coal derived oil, aromatic hydrocarbons (such as benzene, toluene, xylene fractions), coal tar, cycle gas oil from fluid-catalytic-cracking operations, furfural extract of coker gas oil, and mixtures thereof.
  • Waste hydrocarbon motor oil may also be used as a liquid solvent.
  • Hydrocarbon oils having the following properties are suitable: initial atmospheric boiling point greater than 500° F.; Neutralization No., mg KOH/g 0.70 to 1.0; and Aniline point °F. 100 to 110.
  • Other suitable oils comply with ASTM specification D2226, Types 101 and 102.
  • the expression "A and/or B" is used herein in its usual manner and means A or B or A and B.
  • FIG. 1 gives a breakdown of 1991 sales in the United States of solid carbonaceous plastics.
  • the solid carbonaceous plastic-containing material that contains associated inorganic matter e. g. filler or reinforcement material has a higher heating value (HHV) in the range of about 3000 to 19,000 BTU per lb of solid carbonaceous plastic-containing material.
  • the plastic-containing material is granulated by conventional means to a maximum particle dimension of about 1/4", such as about 1/8". Granulating is the preferred method for reducing the size of plastic. Any conventional plastic granulator and mill may be used. For example, a granulator will readily shred/grind solid plastic pieces to a particle size which passes through ASTM E11 Alterative Sieve Designation 1/4" or less.
  • a mill can take the product from the granulator (i.e., -1/4") and readily convert it to smaller sizes (-1/8" or less), such as ASTM E11 Alternative Sieve Designation No. 7.
  • a suitable granulator and mill are made by Enteleter Inc., 251 Welton St., Hamden, Conn. 06517.
  • the ash content for an as-received granulated sample of automotive crusher plastic residue (ACR) is 58.2 wt %.
  • the granulated solid carbonaceous plastic-containing material is mixed together with a liquid slurrying medium comprising a liquid hydrocarbonaceous solvent to produce a pumpable slurry having a solids content in the range of about 15 to 50 wt. % and having a minimum higher heating value (HHV) of about 4500 BTU/lb. of slurry.
  • a liquid slurrying medium comprising a liquid hydrocarbonaceous solvent
  • the pumpable slurry is introduced into a closed autoclave where the granulated plastic material is directly contacted and heated by said pumpable hydrocarbonaceous liquid solvent which is present in the amount of about 1 to 5 parts by wt. of said hydrocarbonaceous liquid solvent per part by wt. of plastic material.
  • the temperature in the autoclave is in the range of 400° F. to 495° F.
  • the pressure in the autoclave is in the range of 150 psig to 750 psig. Under these conditions condensate formation due to cracking and residue formation due to coking are avoided.
  • Liquefaction of a portion of the plastic by contact with the hot hydrocarbonaceous liquid solvent takes place over a period of time in the range of about 20 min. to 6.0 hrs, such as about 30 minutes.
  • the partial liquefaction of the granulated plastic is continued until a pumpable slurry is produced which when cooled to room temperature and pressure comprises the following ingredients in wt. %:
  • the solubilized plastic is that portion of the granulated plastic material that is liquefied by contact with hydrocarbonaceous liquid solvents.
  • the unsolubilized plastic is that portion of the granulated plastic that remains undissolved after said solvent treatment.
  • the separated inorganic material is that portion of the inorganic material produced by the solvent liquefaction treatment of the granulated plastic material that may be easily separated from the remainder of the slurry by settling, screening, filtering, or centrifuging.
  • the density of the separated inorganic material is greater than 1.2.
  • Typical separated inorganic compounds are selected from the group consisting of silica, alumina, calcium carbonate, and mixtures thereof.
  • oxides and/or sulfides of Na, Ca, Mg, Fe, and mixtures thereof are also included.
  • at least a portion of the separated inorganic material is recycled to the autoclave for additional heating in said hydrocarbonaceous liquid solvent.
  • Unseparated inorganic material is that portion of the inorganic material produced by the solvent liquefaction treatment of the granulated plastic material that remains combined in the slurry and cannot be easily separated from the slurry by settling, screening, filtering, or centrifuging.
  • Typical unseparated inorganic material includes mixtures of the oxides and/or sulfides of the following elements: Al, Ba, Ca, Cu, Fe, K, Mg, Mn, Ni, P, Pb, Si, Sr and Ti.
  • the particle size of the unseparated inorganic material is less than 0.2 mm., which is less than the particle size of the separated inorganic material.
  • the pumpable slurry of granulated solid carbonaceous plastic-containing material and liquid slurrying medium, a temperature moderator e.g. H 2 O, CO 2 , and a stream of free-oxygen containing gas are introduced into the reaction zone of a free-flow unobstructed downflowing vertical refractory lined steel wall pressure vessel where the partial oxidation reaction takes place for the production of synthesis gas, reducing gas, or fuel gas.
  • a typical gas generator is shown and described in coassigned U.S. Pat. No. 3,544,291, which is incorporated herein by reference.
  • a two, three or four stream annular type burner such as shown and described in coassigned U.S. Pat. Nos. 3,847,564, and 4,525,175, which are incorporated herein by reference, may be used to introduce the feedstreams into the partial oxidation gas generator.
  • free-oxygen containing gas for example in admixture with steam, may be simultaneously passed through the central conduit 18 and outer annular passage 14 of said burner.
  • the free-oxygen containing gas is selected from the group consisting of substantially pure oxygen i.e. greater than 95 mole % O 2 , oxygen-riched air i.e. greater than 21 mole % O 2 , and air.
  • the free-oxygen containing gas is supplied at a temperature in the range of about 100° F. to 1000° F.
  • the pumpable slurry of granulated solid carbonaceous plastic-containing material and hydrocarbonaceous liquid solvent is passed into the reaction zone of the partial oxidation gas generator by way of the intermediate annular passage 16 at a temperature in the range of about ambient to 650° F.
  • the burner assembly is inserted downward through a top inlet port of the noncatalytic synthesis gas generator.
  • the burner extends along the central longitudinal axis of the gas generator with the downstream end discharging a multiphase mixture of fuel, free-oxygen containing gas, and temperature moderator such as water, steam, or CO 2 directly into the reaction zone.
  • the relative proportions of fuels, free-oxygen containing gas and temperature moderator in the feedstreams to the gas generator are carefully regulated to convert a substantial portion of the carbon in the slurry, e.g., up to about 90% or more by weight, to carbon oxides; and to maintain an autogenous reaction zone temperature in the range of about 1800° F. to 3500° F.
  • the temperature in the gasifier is in the range of about 2400° F. to 2800° F., so that molten slag is produced.
  • the pressure in the partial oxidation reaction zone is in the range of about 1 to 30 atmospheres.
  • the weight ratio of H 2 O to carbon in the feed is in the range of about 0.2-3.0 to 1.0, such as about 0.5-2.0 to 1.0.
  • the atomic ratio of free-oxygen to carbon in the feed is in the range of about 0.8-1.5 to 1.0, such as about 0.9-1.2 to 1.0.
  • the dwell time in the partial oxidation reaction zone is in the range of about 1 to 15 seconds, and preferably in the range of about 2 to 8 seconds.
  • the composition of the effluent gas from the gas generator in mole % dry basis may be as follows: H 2 10 to 60, CO 20 to 60, CO 2 5 to 60, CH 4 nil to 5, H 2 S+COS nil to 5, N 2 nil to 5, and Ar nil to 1.5.
  • the composition of the generator effluent gas in mole % dry basis may be about as follows: H 2 2 to 20, CO 5 to 35, CO 2 5 to 25, CH 4 nil to 2, H 2 S+COS nil to 3, N 2 45 to 80, and Ar 0.5 to 1.5.
  • Unconverted carbon, ash, or molten slag are contained in the effluent gas stream.
  • the effluent gas stream is called synthesis gas, reducing gas, or fuel gas.
  • synthesis gas comprises mixtures of H 2 +CO that can be used for chemical synthesis; reducing gas is rich in H 2 +CO and is used in reducing reactions; and fuel gas comprises mixtures of H 2 +CO, and may also includes CH 4 .
  • the toxic elements in the inorganic matter in the solid carbonaceous plastic-containing material are captured by the noncombustible constituents present and converted into nontoxic nonleachable slag. This permits the nontoxic slag to be sold as a useful by-product.
  • the cooled slag may be ground or crushed to a small particle size e.g. less than 1/8" and used in road beds or building blocks.
  • the hot gaseous effluent stream from the reaction zone of the synthesis gas generator is quickly cooled below the reaction temperature to a temperature in the range of about 250° F. to 700° F. by direct quenching in water, or by indirect heat exchange for example with water to produce steam in a gas cooler.
  • the cooled gas stream may be cleaned and purified by conventional methods.
  • gasifying plastics that contain halides such as polyvinylchloride, polytetrafluoroethylene, by partial oxidation, the halide is released as hydrogen halide (i.e.
  • the aforesaid pumpable aqueous slurry of plastics and waste oil is partially liquefied in a closed autoclave at a temperature of 475° F. and a pressure of 500 psig for 30 minutes.
  • the pumpable slurry from the autoclave is filtered to remove separable inorganic material and the remaining portion is reacted with about 7 tons per day of oxygen gas by partial oxidation in a conventional free flow noncatalytic gas generator at a temperature of about 2400° F. and a pressure of about 500 psig.
  • Synthesis gas comprising H 2 +CO is produced along with about 3 tons of slag.
  • the slag is a coarse, glassy nonleachable material. If however, the same mixture of plastics were fully combusted in air, the slag may contain toxic elements, e.g. chromium in a leachable form.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Processing Of Solid Wastes (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Compounds Of Unknown Constitution (AREA)
  • Extraction Or Liquid Replacement (AREA)
  • Carbon And Carbon Compounds (AREA)
US08/619,749 1993-10-04 1994-09-30 Liquefaction and partial oxidation of plastic materials Expired - Lifetime US5827336A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US08/619,749 US5827336A (en) 1993-10-04 1994-09-30 Liquefaction and partial oxidation of plastic materials

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US13092193A 1993-10-04 1993-10-04
PCT/US1994/011170 WO1995009901A1 (en) 1993-10-04 1994-09-30 Liquefaction and partial oxidation of plastic materials
US08/619,749 US5827336A (en) 1993-10-04 1994-09-30 Liquefaction and partial oxidation of plastic materials

Related Parent Applications (1)

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US13092193A Continuation 1993-10-04 1993-10-04

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US08/415,153 Expired - Fee Related US5534040A (en) 1993-10-04 1995-03-31 Partial oxidation of partially liquified plastic materials

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US (2) US5827336A (ro)
EP (1) EP0722480B1 (ro)
JP (1) JP2727031B2 (ro)
KR (1) KR0172062B1 (ro)
CN (1) CN1071371C (ro)
AT (1) ATE191925T1 (ro)
AU (1) AU692796B2 (ro)
BR (1) BR9407746A (ro)
CA (1) CA2173245C (ro)
CZ (1) CZ98196A3 (ro)
DE (1) DE69424059T2 (ro)
ES (1) ES2145161T3 (ro)
FI (1) FI111379B (ro)
GE (1) GEP20002213B (ro)
NO (1) NO314189B1 (ro)
NZ (1) NZ275603A (ro)
PL (1) PL177964B1 (ro)
PT (1) PT722480E (ro)
RO (1) RO116295B1 (ro)
RU (1) RU2126438C1 (ro)
SK (1) SK281760B6 (ro)
UA (1) UA44255C2 (ro)
WO (1) WO1995009901A1 (ro)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1099747A2 (de) * 1999-11-11 2001-05-16 Noell-KRC Energie- und Umwelttechnik GmbH Verfahren und Vorrichtung zur Verwertung stickstofforganischer Verbindungen durch Vergasung
US20040002622A1 (en) * 2002-06-28 2004-01-01 Robert Gagnon How to produce crude petroleum from organic wastes by a process called petrolisation

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US5904879A (en) * 1996-07-17 1999-05-18 Texaco Inc Partial oxidation of waste plastic material
WO1998002401A1 (en) * 1996-07-17 1998-01-22 Texaco Development Corporation Partial oxidation of waste plastic material
US5977294A (en) * 1997-05-13 1999-11-02 Prs, Llc Polymer deformulation by solvent solution filtration
GB0211052D0 (en) * 2002-05-15 2002-06-26 Tucker Alan C N Incineration of plastic waste suspended in paraffin gel
RU2497846C1 (ru) * 2012-04-24 2013-11-10 Федеральное государственное бюджетное учреждение науки Байкальский институт природопользования Сибирского отделения Российской академии наук (БИП СО РАН) Способ утилизации отходов политетрафторэтилена
RU2600637C2 (ru) * 2015-03-20 2016-10-27 Федеральное государственное бюджетное учреждение науки Институт органического синтеза им. И.Я. Постовского Уральского отделения Российской академии наук (ИОС УрО РАН) Способ переработки отходов, содержащих термореактивные полимеры
US11286436B2 (en) 2019-02-04 2022-03-29 Eastman Chemical Company Feed location for gasification of plastics and solid fossil fuels
US11447576B2 (en) 2019-02-04 2022-09-20 Eastman Chemical Company Cellulose ester compositions derived from recycled plastic content syngas
DE102020102079B4 (de) 2020-01-29 2022-11-10 Cerdia International GmbH Verfahren zum stofflichen wiederverwenden von celluloseacetathaltigem material und systeme zum stofflichen wiederverwenden von celluloseacetathaltigem material
KR20220164602A (ko) * 2020-04-13 2022-12-13 이스트만 케미칼 컴파니 폐 플라스틱을 액화시키고 탈할로겐화시키는 방법
EP4136195A1 (en) * 2020-04-13 2023-02-22 Eastman Chemical Company Vitrification materials to partial oxidation gasifier
CN113308282A (zh) * 2021-05-19 2021-08-27 山东华鲁恒升化工股份有限公司 一种水煤浆及其制备方法和应用

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FI961366A0 (fi) 1996-03-25
SK281760B6 (sk) 2001-07-10
ATE191925T1 (de) 2000-05-15
CN1135768A (zh) 1996-11-13
NO961292D0 (no) 1996-03-29
JP2727031B2 (ja) 1998-03-11
KR0172062B1 (en) 1999-03-20
FI111379B (fi) 2003-07-15
PT722480E (pt) 2000-09-29
EP0722480A1 (en) 1996-07-24
CA2173245A1 (en) 1995-04-13
ES2145161T3 (es) 2000-07-01
GEP20002213B (en) 2000-08-25
EP0722480A4 (en) 1997-03-19
AU7963494A (en) 1995-05-01
DE69424059T2 (de) 2000-09-07
AU692796B2 (en) 1998-06-18
NO961292L (no) 1996-03-29
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BR9407746A (pt) 1997-02-12
JPH09500686A (ja) 1997-01-21
RU2126438C1 (ru) 1999-02-20
EP0722480B1 (en) 2000-04-19
PL313794A1 (en) 1996-07-22
WO1995009901A1 (en) 1995-04-13
SK41396A3 (en) 1997-06-04
FI961366A (fi) 1996-05-24
RO116295B1 (ro) 2000-12-29
UA44255C2 (uk) 2002-02-15
CZ98196A3 (en) 1996-10-16
CA2173245C (en) 1999-06-15
NZ275603A (en) 1996-10-28
PL177964B1 (pl) 2000-02-29
CN1071371C (zh) 2001-09-19
US5534040A (en) 1996-07-09

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